Slightly crosslinked, water-soluble polymaleic acid, its preparation and its use

ABSTRACT

Slightly crosslinked, water-soluble polymaleic acid which is obtainable by polymerization of maleic anyhdride with from 0.1 to 10% by weight of a crosslinking agent in an aromatic hydrocarbon at from 60 to 200° C. in the presence of from 1 to 20% by weight, based on maleic anhydride, of a peroxyester, and hydrolysis of the polymer to give slightly crosslinked polymaleic acid having a Fikentscher K value of from 8 to 20 (measured at 20° C. in 5% strength aqueous solution at pH 7 as the Na salt), a process for the preparation of slightly cross-linked polymaleic acid, and its use as a water treatment agent for reducing boiler scale and hard water deposits in water-conveying systems.

British Pat. No. 1,024,725 discloses a process for the preparation ofpolymaleic anhydride, in which maleic anhydride is polymerized in aninert solvent, for example a dialkyl ether, tetrahydrofuran, dioxane,benzene or a chlorohydrocarbon, such as chloroform, in the presence ofan organic percarbonate or diacyl peroxide. Particularly preferredsolvents are benzene and chloroform. Polymerization initiators used are,for example, diisopropyl percarbonate, dibenzoyl peroxide anddicyclohexyl percarbonate, in amounts of from 2 to 40% by weight, basedon maleic anhydride. The polymers thus prepared contain substantialamounts of unpolymerized maleic anhydride.

In the process of British Patent 1,411,063, polymaleic anhydride isobtained by polymerization of maleic anhydride in xylene as the solvent,which contains up to 99% of ortho-xylene, di-tert-butyl peroxide beingused as the polymerization initiator, in an amount of from 15 to 40% byweight, based on maleic anhydride. The polymers prepared by this processalso contain a substantial amount of unpolymerized maleic anhydride.

U.S. Pat. No. 3,810,834 discloses that hydrolyzed polymaleic anhydrideshaving a molecular weight of from 300 to 5,000 before the hydrolysis orwater-soluble salts of such hydrolyzed polymaleic anhydrides are used inthe water treatment, boiler scale formation being reduced and in manycases virtually completely prevented. The polymers suitable for thispurpose are prepared by polymerization of maleic anhydride in tolueneusing benzoyl peroxide, followed by hydrolysis of the resultingpolymaleic anhydride. Since the polymerization of the maleic anhydrideis not complete and separation of unpolymerized maleic anhydride fromthe polymer is difficult, the polymaleic acids contain substantialamounts of maleic acid.

It is an object of the present invention to provide water-solublepolymaleic acids which nave a broader molecular weight distribution thanthe polymaleic acids known to date, and a process for the preparation ofthese polymaleic acids, in which polymers are obtained whose content offree maleic acid is substantially lower than the maleic acid content ofthe known polymaleic acids. It is a further object of the presentinvention to provide products for reducing boiler scale or hard waterdeposits in water-conveying systems, the said products being moreeffective than polymaleic acids used to date.

We have found that these objects are achieved, according to theinvention, by a slightly crosslinked, water-soluble polymaleic acidwhich is obtainable by polymerization of maleic anhydride with from 0.1to 10% by weight, based on maleic anhydride, of a crosslinking agentcontaining 2 or more ethylenically unsaturated double bonds in anaromatic hydrocarbon at from 60° to 200° C. in the presence of from 1 to20% by weight, based on maleic anhydride, of a peroxyester derived froma saturated or ethylenically unsaturated carboxylic acid, and hydrolysisof the polymer containing anhydride groups to give slightly crosslinkedpolymaleic acid having a Fikentscher K value of from 8 to 20 (measuredin aqueous solution at pH 7 as the sodium salt and at a polymerconcentration of 5% by weight). The slightly crosslinked, water-solublepolymaleic acids are effective agents in the treatment of water for theprevention of boiler scale formation or hard water deposits inwater-conveying systems.

The slightly crosslinked, water-soluble polymaleic acids are obtained bypolymerization of maleic anhydride in the presence of from 0.1 to 10% byweight, based on maleic anhydride, of a crosslinking agent in anaromatic hydrocarbon or a mixture of such hydrocarbons. Examples ofsuitable aromatic hydrocarbons are benzene, toluene, xylene,ethylbenzene, o-, m- and p-diethylbenzene, isopropylbenzene,n-propylbenzene, p-diisopropylbenzene and tetralin. The isomers ofxylene (o-, m- and p-xylene) can be used either in pure form or in theform of mixtures which are commercially available as industrial xylene.Preferably used aromatic hydrocarbons are toluene and o-xylene.

Suitable crosslinking agents are monomers which contain 2 or moreethylenically unsaturated, nonconjugated double bonds. Examples ofsuitable crosslinking agents of this type are diacrylates anddimethacrylates of dihydric or polyhydric saturated alcohols, eg.ethylene glycol diacrylate, ethylene glycol dimethacrylate,1,2-propylene glycol diacrylate, 1,2-propylene glycol dimethacrylate,butane-1,4-diol diacrylate, butane-1,4-diol dimethacrylate, hexanedioldiacrylate, hexanediol dimethacrylate, neopentylglycol diacrylate,neopentyl glycol dimethacrylate, 3-methylpentanediol acrylate and3-methylpentanediol dimethacrylate. Other suitable crosslinking agentsare the acrylates and methacrylates of alcohols containing more than 2OH groups, eg. trimethylolpropane triacrylate or trimethylolpropanetrimethacrylate. Another class of crosslinking agents comprisesdiacrylates and dimethacrylates of polyethylene glycols or polypropyleneglycols, each having molecular weights of from 200 to 9,000.Polyethylene glycols and polypropylene glycols which are used for thepreparation of the diacrylates or dimethacrylates each preferably have amolecular weight of from 400 to 2,000. In addition to the homopolymersof ethylene oxide and propylene oxide, it is also possible to use blockcopolymers of ethylene oxide and propylene oxide or copolymers of these,which contain the ethylene oxide and propylene oxide units in randomdistribution. The oligomers of ethylene oxide and propylene oxide arealso suitable for the preparation of the crosslinking agents, examplesbeing diethylene glycol diacrylate, diethylene glycol dimethacrylate,triethylene glycol diacrylate, triethylene glycol dimethacrylate,tetraethylene glycol diacrylate and/or tetraethylene glycoldimethacrylate. Other suitable crosslinking agents are vinyl esters ofethylenically unsaturated C₃ -C₆ -carboxylic acids, e.g. vinyl acrylate,vinyl methacrylate or vinyl itaconate. Suitable crosslinking agents are,furthermore, vinyl esters of saturated carboxylic acids containing 2 ormore carboxyl groups and di- and polyvinyl ethers of dihydric orpolyhydric alcohols, e.g. divinyl adipate, butanediol divinyl ether andtrimethylolpropane trivinyl ether. Other crosslinking agents are allylesters of ethylenically unsaturated carboxylic acids, e.g. allylacrylate and allyl methacrylate, allyl ethers of polyhydric alcohols,e.g. pentaerithritol triallyl ether, triallyl sucrose and pentaallylsucrose. Methylenebisacrylamide, methylenebismethacrylamide,divinylethyleneurea, divinylpropyleneurea, divinylbenzene,divinyldioxane, tetraallylsilane and tetravinylsilane are also suitablecrosslinking agents.

The crosslinking agents can be used either alone or in the form ofmixtures for the polymerization of the maleic anhydride. They arepreferably employed in an amount of from 0.2 to 5% by weight, based onmaleic anhydride. Preferred crosslinking agents are diacrylates anddimethacrylates derived from polyethylene glycols and/or polypropyleneglycols having a molecular weight of from 400 to 2,000.

Polymerization initiators used according to the invention areperoxyesters formally derived from saturated or ethylenicallyunsaturated carboxylic acids. The primary esters of the peracids aregenerally prepared by reacting the barium salts of primary alkylhydroperoxides with acyl chlorides, while the tertiary alkyl esters ofperacids are obtainable by the simultaneous addition of a dilute alkaliand an acyl chloride to a tert-alkyl hydroperoxide. The carboxylic acidmoiety of the peroxyester molecule is derived from saturated C₁ -C₁₈-carboxylic acids or from ethylenically unsaturated C₃ -C₁₈ -carboxylicacids, preferably from saturated or ethylenically unsaturated carboxylicacids of 4 to 10 carbon atoms. The suitable peroxyesters can berepresented in a simplified manner by the following formulae: ##STR1##

In formulae I and II, R¹ is a saturated C₁ -C₁₇ -alkyl radical or arylradical, H or an ethylenically unsaturated C₂ -C₁₇ -alkenyl radicalwhich may furthermore carry a carb-oxyl group, and R is C₃ -C₂₂ -alkylor an alkyl group which has one or more aromatic substituents, e.g. thecumyl group. R may furthermore be alkylene and is preferably tert-butylor tert-amyl.

Examples of suitable alkyl and aralkyl peroxyesters of carboxylic acidsare cumyl perneodecanoate, tert-butyl perneodecanoate, tert-amylperneodecanoate, tert-amyl perpivalate, tert-butyl perpivalate,tert-butyl perneohexanoate, tert-butyl perisobutyrate, tert-butylper-2-ethylhexanoate, tert-butyl perisononanoate, tert-butyl permaleate,tert-butyl- perbenzoate, 2,5-dimethylhexane 2,5-diperbenzoate andtert-butyl per-3,5,5-trimethylhexanoate. The stated alkyl peresters canbe used either alone or as a mixture in the polymerization. Preferably,tert-butyl perpivalate, tert-butyl per-2-ethylhexanoate or tert-butylperbenzoate is used as the sole initiator or these peroxyester s areused as a mixture with one another or with other alkyl peroxyesters. Theperoxyesters are used in an amount of from 1 to 20, preferably from 5 to16, % by weight, based on the maleic anhydride employed in thepolymerization.

The slightly crosslinked, water-soluble polymaleic acid is prepared intwo stages. In the first process stage, maleic anhydride in an aromatichydrocarbon is polymerized in the presence of from 0.1 to 10% by weight,based on maleic anhydride, of a crosslinking agent containing 2 or moreethylenically unsaturated, nonconjugated bonds, in an aromatichydrocarbon, at from 60° to 200° C., in the presence of theabovementioned peroxyesters. The concentration of the maleic anhydridein solution in the aromatic hydrocarbon is from 20 to 80, preferablyfrom 30 to 70, % by weight, i.e. from 0.25 to 4, preferably from 0.43 to2.33, parts by weight of an aromatic hydrocarbon are used per part byweight of maleic anhydride. The polymerization is preferably carried atfrom 80° to 150° C. For fairly small batches where the resulting heat ofpolymerization can readily be removed, it is possible to polymerize asolution of maleic anhydride and a crosslinking agent in an aromatichydrocarbon by adding a peroxyester and heating the mixture to atemperature in the stated range. On the other hand, it is moreadvantageous if a solution of maleic anhydride and the crosslinkingagent in one or more aromatic hydrocarbons is initially taken in areactor and heated to the temperature required for the polymerization,and the peroxyester, dissolved in an aromatic solvent or an inertsolvent, is metered in continuously or a little at a time according tothe progress of the polymerization reaction. In another version of theprocess, the aromatic hydrocarbon is heated to a temperature in theabovementioned range, and maleic anhydride, the crosslinking agent andthe polymerization initiator are fed in continuously or batchwise at therate at which the polymerization proceeds.

However, the polymerization can also be carried out as follows: some ofthe mixture to be polymerized, for example from 5 to 10% of the totalbatch, is heated to 60°-200° C. in a polymerization reactor so that thepolymerization begins, and the remainder of the components to bepolymerized are then fed continuously or batchwise to the initiallytaken mixture heated at the polymerization temperature, either in theform of a mixture (mixture of maleic anhydride, crosslinking agent andperoxyester, dissolved in an aromatic hydrocarbon) or in the form ofsolutions of maleic anhydride and crosslinking agent or solutions of oneor more peroxyesters in an aromatic hydrocarbon. The polymerization ispreferably carried out under an inert gas atmosphere, for example undernitrogen. In order to remove the heat formed during the polymerization,it is technically simplest to carry out the polymerization at theboiling point of the aromatic hydrocarbon, because the heat ofpolymerization can then be removed from the system by means ofevaporative cooling. The use of mixtures of several aromatichydrocarbons makes it possible to set the of polymerizationtemperatures. Another possible method of carrying out the polymerizationat the boiling point of the particular aromatic hydrocarbon used or of amixture of aromatic hydrocarbons is to carry out the polymerizationunder reduced or superatmospheric pressure, depending on the desiredpolymerization temperature. In addition to the substantially batchwisepolymerizations described above, the process can also be carried outcontinuously for the preparation of relatively large amounts of slightlycrosslinked, water-soluble polymaleic anhydride. For the continuouspolymerization, a cascade of two or more polymerization reactorsconnected in series is required in most cases. In a continuous process,monomer feeds of different compositions are metered continuously intothe first two reactors. In this procedure, it is also possible to feedthe total amount of monomers to the first reactor and to distribute therequired amounts of initiator over 2 or 3 reactors.

In order to prepare polymers having a particularly low residual monomercontent, the main polymerization can be followed by a subsequentpolymerization which is carried out either at the same temperature asthe main polymerization or at a temperature which is from 10° to 40° C.higher. Peroxyesters are preferably used in the subsequentpolymerization, a total of from 1 to 20% by weight of the peroxyesterbeing required for the main and subsequent polymerizations. In the mainpolymerization, it is possible to use the total amount of peroxyesterand then carry out the subsequent polymerization or to use from 80 to95% of the required amount of initiator in the main polymerization and,when the latter is complete, to add the remaining amount of initiatorand carry out subsequent polymerization.

The crosslinking agents polymerize virtually completely under thereaction conditions. The conversion of maleic anhydride is higher than99%, so that slightly crosslinked polymers of maleic anhydride whichcontain less than 1% by weight of unpolymerized maleic anhydride areobtained. The structure of the said polymers is not known. However, thebalance of quantities, the elemental analysis and the IR spectraindicate that the slightly crosslinked polymer contains not onlypolymerized maleic anhydride and polymerized crosslinking agent but alsothe particular aromatic hydrocarbon used and decomposition products ofthe peroxyesters in bound form. Up to 75, preferably from 10 to 65, % byweight, based on maleic acid, of aromatic hydrocarbon and decompositionproducts of the initiator are incorporated into the slightly crosslinkedpolymaleic acid if it is assumed that conversion of maleic anhydride topolymaleic anhydride is 100%. The polymerization of the maleic anhydridein the presence of from 0.1 to 10% by weight of crosslinking agentsaccording to the invention gives, depending on the choice of solvent,clear polymer solutions (for example in ethylbenzene) or precipitates ofthe polymers or two separate phases, each containing polymer and thelower phase having an oily consistency at above 90° C. and solidifyingon cooling. The upper phase essentially consists of a solution (forexample in the case of polymerization in xylene). The polymers, whichare present in the two different phases, have different performancecharacteristics. However, they can both be used together for the samepurpose and therefore need not be separated. However, it is alsopossible to carry out separation or fractionation of the polymer batch,in which case particularly effective water treatment agents can beprepared. The aromatic hydrocarbons not incorporated into the polymerduring the polymerization can be recovered and reused for thepolymerization, even without purification. The polymerization of themaleic anhydride with the crosslinking agents is carried out in theabsence of water. The aromatic hydrocarbons used in the polymerizationare virtually anhydrous or contain no more than 0.2% by weight of water,i.e. amounts of water which, when the water is in contact with thearomatic hydrocarbon, are dissolved therein.

In a second process step, the products prepared in the polymerizationare hydrolyzed. For this purpose, water can be added to prepare polymersin the acid form and the reaction mixture can be heated to 70°-150° C.in order to complete the hydrolysis of the anhydride groups of thecrosslinked polymer. If the hydrolysis of the polymer is carried out atabove the boiling points of the solvent/water mixtures, the reaction iscarried out under super-atmospheric pressure. The aromatic hydrocarbonused in the polymerization can be distilled off from the resultingaqueous polymer solution before or after the hydrolysis. However, thepolymers can also be precipitated from the reaction mixture obtained inthe polymerization, by adding a solvent in which they are insoluble, andcan then be hydrolyzed.

If desired, the aqueous solution of the slightly crosslinked polymaleicacid can be neutralized with an alkali, ammonia or an amine. To preparethe salts of the said polymaleic acid, it is preferable if the reactionmixture obtained in the polymerization is neutralized with an aqueoussolution of an alkali metal base, ammonia or an amine. In these casestoo, the aromatic hydrocarbon can be distilled off during or after theneutralization or reused. In all cases, aqueous solutions of salts of aslightly crosslinked polymaleic acid are obtained. Preferably usedalkali metal bases are sodium hydroxide solution and potassium hydroxidesolution. The neutralization can also be effected with ammonia or anamine, e.g. triethylamine, hexylamine, ethanolamine, triethanolamine ormorpholine. However, the hydrolysis of the anhydride groups of theslightly crosslinked polymer can be carried out not only with water butalso with aqueous solutions of bases or acids. If the slightlycrosslinked polymers of maleic acid in the acid form arewater-insoluble, they are converted by neutralization with a base intothe alkali metal salt, which is water-soluble.

The K value of the slightly crosslinked, water-soluble polymaleic acidsis from 7 to 20, preferably from 8.5 to 15 (determined as the sodiumsalt in 5% strength aqueous solution at 25° C. and pH 7). The saidpolymaleic acids contain less than 1% by weight of monomeric maleic acid(determined polarographically). The aqueous solutions of the hydrolyzedpolymers can therefore be used directly, without further purification,to reduce or suppress scaling or hard water deposits in water-conveyingsystems.

The mode of action of these scale inhibitors consists in preventing theformation of crystals of the salts causing hardness, such as calciumcarbonate, magnesium oxide, magnesium carbonate, calcium, barium andstrontium sulfate, calcium phosphate (apatite) and the like, whenmetered in substoichiometric amounts, or in influencing the formation ofthese precipitates in such a way that, instead of hard and stone-likedeposits, precipitates which are readily washed away and are finelydistributed in the water are formed. In this way, the surfaces of, forexample, heat exchangers, pipes and pump components are kept free ofdeposits and their tendency to corrosion is reduced. In particular, thedanger of pitting under these deposits is reduced, and, furthermore, thegrowth of microorganisms on these metal surfaces is inhibited. As aresult of the effect of these scale inhibitors, the life of such systemscan be increased and down times for cleaning parts of the system can besubstantially reduced. The amounts of scale inhibitor required for thispurpose are only from 0.1 to 100 ppm, based on the particular amount ofwater. The water-conveying systems are, for example, open or closedcooling circulations, for example in power stations or chemical plants,such as reactors, distillation apparatuses and similar components, inwhich heat has to be removed. These scale inhibitors can also be used inboiler waters and steam generators, preferably at water temperaturesbelow 150° C. Another preferred application of the novel scaleinhibitors is for the desalination of sea water and brackish water bydistillation or membrane processes, for example reverse osmosis orelectrodialysis. For example, in the MSF distillation process for thedesalination of sea water, concentrated sea water is circulated atelevated temperatures. The novel scale inhibitors effectively suppressthe precipitation of salts causing hardness, such as brucite, and cakingof these salts on plant components.

In membrane processes, damage to the membranes by crystallizinghardness-producing salts can be effectively prevented. These scaleinhibitors thus permit higher concentration factors, improved yield ofpure water and longer membrane lives. Another application of these scaleinhibitors is, for example, in the concentration of sugar cane or sugarbeet liquors. In contrast to the applications described above, in thiscase, for example, calcium hydroxide, carbon dioxide, sulfur dioxide or,if appropriate, phosphoric acid is added to the clarified juice toeffect purification. Sparingly soluble calcium salts, e.g. calciumcarbonate, sulfate or phosphate, which remain in the sugar liquor afterfiltration, are then precipitated during the concentration process andmay occur as stone-hard deposits on heat exchanger surfaces. This alsoapplies to impurities in the sugar, such as silica or calcium salts oforganic acids such as oxalic acid.

The same applies to processes which follow the sugar recovery, forexample the production of alcohol from residues obtained in sugarproduction.

The novel scale inhibitors are capable of substantially suppressing theformation of these deposits, so that down times for cleaning the plant,for example by boiling, can be substantially reduced. Another importantaspect here is the considerable energy saving as a result of avoidingthe said heat-insulating deposits.

The amounts of scale inhibitor which are required for the applicationsdescribed are variable but are from 0.1 to 100 ppm, based on the coolingwater, boiler water or process water used or, for example, on the sugarliquor.

The hydrolyzed crosslinked polymers of maleic acid can furthermore beincorporated into detergent formulations as incrustation inhibitors andantiredeposition agents in an amount of from 0.5 to 10% by weight. Theslightly crosslinked water-soluble polymaleic acids are also suitable aswater hardness stabilizers in cleaner formulations. They are alsosuitable, in an amount of from 0.1 to 5% by weight, as dispersants forpigments, for example for the production of highly concentrated aqueoussuspensions of clay or chalk for the preparation of paper coating slips.

In the Examples, parts and percentages are by weight. The K values ofthe hydrolyzed polymers were determined according to H. Fikentscher,Cellulose-Chemie, 13 (1932), 48-64 and 71-74, in aqueous solution at pH7, 25° C. and a concentration of the sodium salt of the polymer of 5% byweight.

EXAMPLE 1

A solution of 400 g of maleic anhydride and 8 g of butanediol diacrylatein 600 g of o-xylene is heated to 146° C. (refluxing) in a 2 l glassreactor provided with a stirrer, a thermometer, a nitrogen inlet, acondenser, feed vessels and an apparatus for passing in steam. As soonas the solution begins to boil, a solution of 60 g of tert-butylper-2-ethylhexanoate in 100 g of o-xylene is metered in over 5 hours.The polymerization is carried out under reflux with thorough mixing. Thetemperature falls from 146° C. to 140° C. in the course of thepolymerization. When the addition of initiator is complete, the reactionmixture is heated at the boil for a further hour and hen cooled to 97°C. and hydrolyzed by adding 300 g of water. Steam is then passed intothe reaction mixture, and the unconverted o-xylene is removedazeotropically. A clear yellow aqueous solution having a solids contentof 61% remains. The slightly crosslinked polymaleic acid has a K valueof 9.7 in the form of the sodium salt. The residual monomer content,based on the solids content, is 0.16% of maleic acid. The yield of thesaid polymaleic acid is 129%, based on maleic acid, the amount of whichis calculated from the maleic anhydride used.

EXAMPLE 2

Example 1 is repeated, except that the amount of crosslinking agent isincreased to 20 g. A brown, virtually clear aqueous solution having asolids content of 64.5% is obtained. The slightly crosslinked polymaleicacid has a K value of 10.3 in the form of the sodium salt. The residualmonomer content, based on the solids content, is 0.36% of maleic acid.The yield of the said polymaleic acid is 132%, based on maleic acid, theamount of which is calculated from the maleic anhydride used.

EXAMPLE 3

Example 1 is repeated, except that, instead of the amount ofcrosslinking agent used there, 40 g of butanediol diacrylate is nowemployed. A brown cloudy aqueous solution having a solids content of584% is obtained. The slightly crosslinked polymaleic acid has a K valueof 11.9 in the form of the sodium salt. The residual monomer content,based on the solids content, is 0.45% of maleic acid. The yield ofslightly crosslinked, water-soluble polymaleic acid is 134%, based onmaleic acid, the amount of which is calculated from the maleic anhydrideused.

EXAMPLE 4

A solution of 400 g of maleic anhydride and 20 g of a diacrylate of apolyethylene glycol having a molecular weight of 1500 in 600 g ofo-xylene is heated at the boil in the apparatus described in Example 1,and a solution of 60 g of tert-butyl per-2-ethylhexanoate in 100 g ofo-xylene is added under a nitrogen atmosphere and with stirring, in thecourse of 5 hours. When the addition of the initiator is complete, thereaction mixture is heated at the boil for a further hour to continuethe polymerization and then cooled to 95° C. At this temperature, 300 gof water are then added, and the unpolymerized o-xylene is removed bypassing in steam. A brown aqueous solution having a solids content of60% remains. The slightly crosslinked polymaleic acid has a K value of10.1 in the form of the sodium salt. The residual monomer content, basedon the solids content, is 0.17% of maleic acid. The yield of the saidpolymaleic acid is 128%, based on maleic acid, the amount of which iscalculated from the maleic anhydride used.

EXAMPLE 5

Example 4 is repeated, except that the amount of crosslinking agent isincreased to 40 g. Here too, the diacrylate of a polyethylene glycolhaving a molecular weight of 1500 is used as the crosslinking agent. Abrown aqueous solution of a slightly crosslinked polymaleic acid isobtained. The solids content of the aqueous solution is 56.9%. The saidpolymaleic acid has a K value of 10.7 in the form of the sodium salt.The residual monomer content, based on the solids content, is 0.19% ofmaleic acid. The yield of the said polymaleic acid is 132%, based onmaleic acid, the amount of which is calculated from the maleic anhydrideused in the polymerization.

COMPARATIVE EXAMPLE 1

A stirred solution of 300 g of maleic anhydride in 300 g of industrialxylene is refluxed in the polymerization reactor stated in Example 4. Assoon as the solution begins to boil, a solution of 100 g ofdi-tert-butyl peroxide, dissolved in 150 g of industrial xylene, isadded continuously in the course of 2 hours. As the polymerizationprogresses, the boiling point of the reaction mixture falls from 136° C.to 125° C. When the addition of the initiator is complete, the reactionmixture is polymerized for a further 4 hours at 125° C., cooled to 95°C. and then hydrolyzed by adding 300 g of water. The aromatichydrocarbons used as solvents and not incorporated in the polymer areremoved azeotropically by passing in steam. A clear brown aqueoussolution of polymaleic acid having a solids content of 48.7% isobtained. The polymaleic acid has a K value of 10.1 in the form of thesodium salt. The content of unpolymerized maleic acid is 4.1%, based onthe solids content of the aqueous solution.

COMPARATIVE EXAMPLE 2

Comparative Example 1 is repeated, except that, instead of the initiatorsolution used there, a solution of 45 g of di-tert-butyl peroxide in 150g of industrial xylene is now employed. This gives a deep brown clearaqueous solution which contains 86%, based on the solids content, ofunpolymerized maleic acid.

COMPARATIVE EXAMPLE 3

A solution of 300 g of maleic anhydride in 300 g of o-xylene ispolymerized in the apparatus stated in Example 4. The maleic anhydridesolution in xylene is heated to the boil, and a solution of 100 g ofdi-tert-butyl peroxide in 150 g of o-xylene is added continuously at theboiling point in the course of 2 hours. As the polymerization proceeds,the boiling point of the reaction mixture falls from 146° C. to 127° C.When the addition of the initiator is complete, the reaction mixture isrefluxed for a further 4 hours and then cooled to 95° C., and 300 g ofwater are added to effect hydrolysis. The o-xylene used as the solventis then removed by steam distillation. A clear brown aqueous solution ofpolymaleic acid, having a solids content of 62.4%, is obtained. Theresidual monomer content is 18.5%, based on solids.

COMPARATIVE EXAMPLE 4

A solution of 877 g of maleic anhydride in 877 g of industrial xylene isrefluxed in a 4 1 reactor provided with a stirrer, a thermometer, anitrogen inlet, a condenser, a feed vessel and an apparatus for passingin steam. As soon as the solution begins to boil, a solution of 292 g oftert-butyl hydroperoxide in 350 g of industrial xylene is addedcontinuously under a nitrogen atmosphere and with constant stirring, inthe course of 2 hours. When the addition of the initiator is complete,the mixture is heated at the boil for a further 4 hours and then cooledto 96° C., 600 g of water are added and the mixture is then subjected tosteam distillation in order to remove the industrial xylene. A clearbrown aqueous solution having a solids content of 55.9% results. Thecontent of unpolymerized maleic acid is 10.5%, based on the solidscontent.

COMPARATIVE EXAMPLE 5

A solution of 100 g of maleic anhydride in 100 g of industrial xylene isheated at the boil under nitrogen and with stirring in the apparatusdescribed in Example 1, and a solution of 15 g of tert-butylhydroperoxide in 50 g of industrial xylene is added continuously in thecourse of 2 hours. When the addition of the initiator is complete, thereaction mixture is heated at the boil for a further 4 hours and thencooled to 94° C., 50 g of water are added and the mixture is subjectedto steam distillation. A clear brown solution having a solids content of56.5% is obtained. The content of unpolymerized maleic acid is 34.2%,based on the solids content.

COMPARATIVE EXAMPLE 6

Comparative Example 5 is repeated, except that, instead of the initiatorsolution used there, a solution of 15 g of dicumyl peroxide in 50 g ofindustrial xylene is now used. A clear brown aqueous solution having asolids content of 54.3% is obtained. The content of maleic acid in thepolymer solution is 30%, based on the solids content.

COMPARATIVE EXAMPLE 7

A solution of 400 g of maleic anhydride in 600 g of o-xylene isinitially taken in the apparatus described in Example 4 and heated atthe boil with stirring in a stream of nitrogen. As soon as the solutionbegins to boil, a solution of 60 g of dilauroyl peroxide in 200 g ofo-xylene is metered in continuously in the course of 5 hours. When theaddition of the initiator is complete, the reaction mixture is heated atthe boil for a further hour and then cooled to 95° C., and 300 g ofwater are added to hydrolyze the polymer. The unconverted o-xylene isremoved by steam distillation. A clear yellow aqueous solution having asolids content of 51% results. The aqueous solution contains 23%, basedon the solids content, of maleic acid.

COMPARATIVE EXAMPLE 8

A solution of 100 g of maleic anhydride in 233 g of industrial xylene isheated to the boil, under nitrogen and with thorough mixing, in theapparatus described in Comparative Example 5, and, when the solutionbegins to boil, a solution of 7.5 g of 2,2'-azobisisobutyronitrile in 50of industrial xylene is added in the course of 2 hours. Thepolymerization is carried out at the boiling point of the reactionmixture. When the addition of the initiator is complete, the reactionmixture is heated at the boil for a further 4 hours and then cooled to97° C., 50 g of water are added and the mixture is subjected to steamdistillation. A clear reddish brown aqueous solution having a solidscontent of 54.2% results. The aqueous polymer solution contains 13.3%,based on the solids content, of maleic acid.

COMPARATIVE EXAMPLE 9

Comparative Example 8 is repeated, except that a solution of 7.5 g of2,2'-azobis-(2,4-dimethylvaleronitrile) in 50 g of industrial xylene isused as the polymerization initiator. A clear reddish brown aqueouspolymer solution having a solids content of 56.3% is obtained. Thecontent of maleic acid is 42.9%, based on the solids content.

COMPARATIVE EXAMPLE 10

Comparative Example 7 is repeated, except that, instead of the initiatorsolution described there, an initiator solution consisting of 60 g ofmethyl ethyl ketone peroxide in 100 g of o-xylene is employed. Ablackish brown aqueous solution having a solids content of 53.1% isobtained. The aqueous solution contains 78.4%, based on the solidscontent, of maleic acid.

The Comparative Examples clearly show that the polymerization initiatorspreviously described for the polymerization of maleic anhydride givepolymers having a high residual monomer content. The residual monomercontent of the aqueous polymer solutions obtained according toComparative Examples 2 to 10 were so high that it was impossible todetermine the K value. However, the Comparative Examples also show thatsubstantial amounts of di-tert-butyl peroxide are required for thepolymerization of maleic anhydride before a more or less satisfactoryconversion is obtained in the polymerization. In contrast, a conversionwhich is higher than 99% is obtained using the peroxyesters according tothe present invention in the polymerization of maleic anhydride in thepresence of crosslinking agents. The content of maleic acid in thehydrolyzed products was less than 1% in every case. The high conversionin the novel process and the low content of maleic acid in thehydrolyzed, slightly crosslinked polymers is surprisingly achieved witha smaller amount of initiator compared with the prior art.

EXAMPLES OF USE Test Methods Dynamic CaCO₃ inhibition

This test simulates the formation of deposits of calcium carbonate in acooling circulation. In this test method, test water with 30° d Cahardness, 10° d Mg hardness and 56° d carbonate hardness is pumped for 2hours through a glass spiral heated at 75° C. (flow rate 0.5 l/h). Thedeposit formed in the spiral is dissolved, and Ca+Mg is determinedcomplexometrically. The inhibitor action is calculated from the amountof deposit in the blank test and in the presence of the correspondingamounts of scale inhibitor.

Dispersing Ca phosphate

This test can be used to determine the dispersant effect on precipitateswhich have separated out. Here, test water containing 500 ppm ofprecipitated calcium phosphate at pH 8.5-9 is kept at 100° C. for 1 hourand then transferred to a cylinder. After 1 hour, the Ca content in themiddle of the cylinder is determined complexometrically. The dispersanteffect is calculated from the amount of dispersed calcium phosphate inthe blank test and in the presence of the dispersant. Screening test,desalination of sea water

Synthetic sea water (200 ml) according to DIN 50,900 (1960), having aninitial salt concentration of 6.15%, is evaporated down at 95° C. untilcloudiness is observed. The volume obtained is a measure of theefficiency of the scale inhibitor.

EXAMPLES 6 TO 8

Using the test methods described above, the calcium carbonate inhibition(dynamic), the dispersing of calcium phosphate and the efficiency in theconcentration of sea water are determined for the slightly crosslinkedpolymaleic acids shown in the Table. For comparison, the properties ofthe polymaleic acid obtained according to Comparative Example 1 aredetermined. The values determined for this are likewise shown in theTable.

                                      TABLE                                       __________________________________________________________________________                                  Dispersing of Ca phosphate,                                                                 Concentration of                         Slightly crosslinked                                                                     CaCO.sub.3 inhibition                                                                     %, for        sea water (volume                        polymaleic acid                                                                          (dynamic) % for   60 ppm of                                                                             in ml at which                    Example                                                                              according to Example                                                                     2 ppm of added polymer                                                                    30 45 added polymer                                                                         cloudiness occurs)                __________________________________________________________________________    6      1          82.2        90.2                                                                             98.4                                                                             99.2    108                               7      2          88.3        56.3                                                                             95.6                                                                             96      104                               8      4          83.3        76.5                                                                             97.2                                                                             97.2    102                                      Polymaleic acid                                                                          68.5         2.1                                                                             55.0                                                                             62.9    129                               Comparative                                                                          according to                                                           Example                                                                              Comparative Example                                                    11     1                                                                      __________________________________________________________________________

We claim:
 1. A process for preparing crosslinked water-solublepolymaleic acid containing less than 1% by weight of unpolymerizedmaleic anhydride consisting of polymerizing maleic anhydride with from0.1 to 10% by weight, based on maleic anhydride, of a crosslinking agentselected from a diacrylate of dimethacrylate of a dihydric of polyhydricsaturated C₂ -C₆ alcohol or a diacrylate or dimethacrylate of apolyethylene or polypropylene glycol having a molecular weight of from250 to 9,000, in an aromatic hydrocarbon at 60° to 200° C., in thepresence of from 1 to 20% by weight, based on maleic anhydride, of aperoxyester polymerization initiator derived from a saturated C₄ -C₁₀carboxylic acid and then hydrolyzing the polymer.
 2. A process asclaimed in claim 1, wherein the polymerization is carried out inbenzene, toluene, xylene, ethylbenzene, diethylbenzene,isopropylbenzene, diisopropylbenzene or a mixture thereof at from 80° to150° C.
 3. A process as claimed in claim 1, wherein the polymerizationinitiator is used in an amount of from 5 to 16% by weight, based onmaleic anhydride.
 4. A process as claimed in claim 1, wherein thecrosslinking agent used is a diacrylate or dimethacrylate of a dihydricsaturated alcohol of 2 to 6 carbon atoms.
 5. A process as claimed inclaim 1, wherein the crosslinking agent used is a diacrylate ordimethacrylate of a polyethylene glycol or a polypropylene glycol havinga molecular weight of from 400 to 2,000.
 6. A process as claimed inclaim 1, wherein the crosslinking agent is used in an amount of from 0.2to 5% by weight, based on maleic anhydride.
 7. A process as claimed inclaim 1, wherein the polymerization initiator used is tert-butylper-2-ethylhexanoate, tert-butyl perpivalate, tert-butyl perbenzoate ora mixture of these.
 8. A process as claimed in claim 1, wherein thepolymerization initiator used is tert-butyl permaleate.